Recycling superabsorbent polymer fines

ABSTRACT

A process is described for recycling superabsorbent polymer fines into a process that includes treating the superabsorbent polymer fines with caustic and a polymerization step for making the superabsorbent polymer gel. The process requires treating the superabsorbent polymer fines with a caustic, followed by mixture with polymerizable monomer solution, and polymerizing the mixture of the superabsorbent polymer fines and monomer to form the aqueous fluid absorbent polymer. In the process, the fines are incorporated into the new polymer gel and become indistinguishable there from. The gel may then be comminuted into a particulate dried and then separated into a portion having a desired minimum particle size in a fines portion having less than the desired size. The particulate may then be coated with a surface crosslinking agent and surface additives and heated for surface conversion.

BACKGROUND

A superabsorbent material in general refers to a water-swellable,water-insoluble, material capable of absorbing at least about 10 timesits weight, and up to about 30 times or more its weight in an aqueoussolution containing 0.9 weight percent sodium chloride solution inwater. The present invention relates to superabsorbent polymerparticles, which absorb water, aqueous liquids, and blood, and a methodto make the superabsorbent polymer and particles. The acronym SAP may beused herein, and is generally used in the industry, in place ofsuperabsorbent polymer, superabsorbent polymer composition,superabsorbent polymer particles, or variations thereof.

A superabsorbent polymer is a cross linked partially neutralized polymerthat is capable of absorbing large amounts of aqueous liquids and bodyfluids, such as urine or blood, with swelling and the formation ofhydrogels, and of retaining them under a certain pressure in accordancewith the general definition of superabsorbent material. A superabsorbentpolymer composition is a superabsorbent polymer that has been surfacetreated that may include surface cross linking, surface treatment, andother treatment. Commercially available superabsorbent polymercompositions include cross linked polyacrylic acids or cross linkedstarch-acrylic acid graft polymers, in which some of the carboxyl groupsare neutralized with sodium hydroxide solution or potassium hydroxidesolution. Superabsorbent polymer composition particles are particles ofsuperabsorbent polymers or superabsorbent polymer compositions, andgenerally have a particle size of from about 150 microns to about 850microns. A comprehensive survey of superabsorbent polymers, and theiruse and manufacture, is given in F. L. Buchholz and A. T. Graham(editors) in “Modem Superabsorbent Polymer Technology,” Wiley-VCH, NewYork, 1998.

A primary use of SAP and SAP particles is in sanitary articles, such asbabies' diapers, incontinence products, or sanitary towels. For fit,comfort, and aesthetic reasons, and from environmental aspects, there isan increasing trend to make sanitary articles smaller and thinner. Thisis being accomplished by reducing the content of the high volume flufffiber in these articles. To ensure a constant total retention capacityof body fluids in the sanitary articles, more SAP content is being usedin these sanitary articles.

The present invention relates generally to superabsorbent polymercomposition particles having a particle size of about 150 microns orless, which are generally known to those skilled in the art and referredherein as superabsorbent polymer fines, SAP fines, or fines. The presentinvention relates to recycling the superabsorbent polymer fines duringthe production process. More particularly, the invention relates toreprocessing superabsorbent polymer fines generated in the production ofsuperabsorbent polymer particles.

In particular, SAP fines are generally generated during the cutting,comminution (pulverization), and grinding steps of the dried polymergel. Superabsorbent polymer fines are considered to be undesirable insanitary articles including infant diapers and adult incontinencedevices. Such SAP fines may migrate in the device before use and exhibitgel blocking in application. In addition, it has been found thatsuperabsorbent polymer particles made including a portion of recycledsuperabsorbent polymer fines have properties including absorption asmeasured by the Centrifuge Retention Capacity test (CRC), absorbencyunder load (AUL), and permeability (GBP) that are less desirous than thesuperabsorbent polymer particles that are made from a process that doesnot include recycling superabsorbent polymer fines.

U.S. Pat. No. 5,514,754 is directed to a process for increasing the sizeof fine particles of SAP (cross-linked polyacrylic acid, cross-linkedpolyacrylate, and/or cross-linked partially neutralized polyacrylicacid) and, more particularly, to a process of impregnating the SAPparticles with an aqueous monomer solution of acrylic acid and/or metalsalts of acrylic acid. Impregnation is achieved by intimately mixing theSAP fines (e.g., having a particle size less than about 300 μm) with themonomer solution to form a paste having a viscosity of, e.g., about20,000 to about 5,000,000 centipoise. Polymerization of a monomerwithin, and drying of, the paste then is achieved, e.g., by heat.

It is an object of the present invention to provide superabsorbentpolymer particle compositions made by a process that includes recycledsuperabsorbent polymer fines wherein the superabsorbent polymer particlecompositions have improved properties including an absorption capacityto retain fluids under no load, high absorption capacities to retainfluid under pressure as measured by absorption under load at 0.9 psi,and improved gel bed permeability.

SUMMARY

An embodiment of the present invention comprises a process for theproduction of a superabsorbent polymer gel with recycled superabsorbentpolymer fines comprising the following steps: a) treating thesuperabsorbent polymer fines with a caustic solution containing fromabout 0.1 to about 12% caustic based on the weight of the superabsorbentpolymer fines; b) mixing the treated superabsorbent polymer finesobtained in step a) with a polymerization solution containing at leastone cross-linking-agent and a partially neutralized monomer in which thecontent of the superabsorbent polymer fines relative to the total amountof the monomer is from about 0.1 to about 30 wt %; and c) polymerizingthe mixture obtained in step b) to produce the superabsorbent polymergel.

In addition the process may further comprise the steps of comminutingthe superabsorbent polymer gel from said polymerizing step; drying saidcomminuted polymer gel; separating said dried superabsorbent polymerparticle composition into a portion having a desired particle size fromabout 150 μm to about 850 μm.

The process may further comprise the steps to make a superabsorbentpolymer composition wherein the steps comprise coating thesuperabsorbent polymer particulate with a surface cross linking agentand surface additives, heating the coated superabsorbent polymercomposition, and separating said dried superabsorbent polymerparticulate into a portion having a desired particle size from about 150 μm to about 850 μm as measured by screening through a U.S. standard20 mesh screen and retained on a U.S. standard 100 mesh screen.

And furthermore, the process may further comprise the steps ofseparating superabsorbent polymer fines having a particle size of lessthan about 150 μm and recycling said superabsorbent polymer fines to thepolymerizing step for forming said superabsorbent polymer compositionparticle.

An embodiment of the present invention further includes a superabsorbentpolymer particulate made by the foregoing process. In addition, thepresent invention is directed to absorbent compositions or sanitaryarticles such as diapers that may contain superabsorbent polymercompositions of the present invention.

It has been found that the caustic treatment on superabsorbent polymerfines increases certain properties of the superabsorbent polymerparticle composition made by a process that incorporates caustic treatedsuperabsorbent polymer fines.

Numerous other features and advantages of the present invention willappear from the following description. In the description, reference ismade to exemplary embodiments of the invention. Such embodiments do notrepresent the full scope of the invention. Reference should therefore bemade to the claims herein for interpreting the full scope of theinvention. In the interest of brevity and conciseness, any ranges ofvalues set forth in this specification contemplate all values within therange and are to be construed as support for claims reciting anysub-ranges having endpoints which are real number values within thespecified range in question. By way of a hypothetical illustrativeexample, a disclosure in this specification of a range of from 1 to 5shall be considered to support claims to any of the following ranges:1-5; 1-4; 1-3; 1-2; 2-5; 2-4; 2-3; 3-5; 3-4; and 4-5.

FIGURES

The foregoing and other features, aspects, and advantages of the presentinvention will become better understood with regard to the followingdescription, appended claims, and accompanying drawings where:

FIG. 1 is a side view of the test apparatus employed for the Free SwellGel Bed Permeability Test;

FIG. 2 is a cross-sectional side view of a cylinder/cup assemblyemployed in the Free Swell Gel Bed Permeability Test apparatus shown inFIG. 1;

FIG. 3 is a top view of a plunger employed in the Free Swell Gel BedPermeability Test apparatus shown in FIG. 1; and

FIG. 4 is a side view of the test apparatus employed for the AbsorbencyUnder Load Test;

DEFINITIONS

It should be noted that, when employed in the present disclosure, theterms “comprises,” “comprising,” and other derivatives from the rootterm “comprise” are intended to be open-ended terms that specify thepresence of any stated features, elements, integers, steps, orcomponents, and are not intended to preclude the presence or addition ofone or more other features, elements, integers, steps, components, orgroups thereof.

The term “absorbent article” generally refers to devices that can absorband contain fluids. For example, personal care absorbent articles referto devices that are placed against or near the skin to absorb andcontain the various fluids discharged from the body.

The term “caustic” or “caustic soda” is used herein to describe achemical that forms an alkaline solution when dissolved in a solventsuch as water, including for example sodium hydroxide, sodium carbonate,or sodium bicarbonate.

The term “cross linked” used in reference to the superabsorbent polymerrefers to any means for effectively rendering normally water-solublematerials substantially water-insoluble but swellable. Such a crosslinking means can include, for example, physical entanglement,crystalline domains, covalent bonds, ionic complexes and associations,hydrophilic associations such as hydrogen bonding, hydrophobicassociations, or Van der Waals forces.

The term “Darcy” is a CGS unit of permeability. One Darcy is thepermeability of a solid through which one cubic centimeter of fluid,having a viscosity of one centipoise, will flow in one second through asection one centimeter thick and one square centimeter in cross-section,if the pressure difference between the two sides of the solid is oneatmosphere. It turns out that permeability has the same units as area;since there is no SI unit of permeability, square meters are used. OneDarcy is equal to about 0.98692×10⁻¹² m² or about 0.98692×10⁻⁸ cm².

The term “disposable” is used herein to describe absorbent articles thatare not intended to be laundered or otherwise restored or reused as anabsorbent article after a single use. Examples of such disposableabsorbent articles include, but are not limited to, personal careabsorbent articles, health/medical absorbent articles, andhousehold/industrial absorbent articles.

The term “dry superabsorbent polymer composition” generally refers tothe superabsorbent polymer composition having less than about 10%moisture.

The term “mass median particle size” of a given sample of particles ofsuperabsorbent polymer composition is defined as the particle size,which divides the sample in half on a mass basis, i.e., half of thesample by weight has a particle size greater than the mass medianparticle size, and half of the sample by mass has a particle size lessthan the mass median particle size. Thus, for example, the mass medianparticle size of a sample of superabsorbent polymer compositionparticles is 2 microns if one-half of the sample by weight is measuredas more than 2 microns.

The terms “particle,” “particulate,” and the like, when used with theterm “superabsorbent polymer,” refer to the form of discrete units. Theunits can comprise flakes, fibers, agglomerates, granules, powders,spheres, pulverized materials, or the like, as well as combinationsthereof. The particles can have any desired shape: for example, cubic,rod-like, polyhedral, spherical or semi-spherical, rounded orsemi-rounded, angular, irregular, et cetera. Shapes having a high aspectratio, like needles, flakes, and fibers, are also contemplated forinclusion herein. The terms “particle” or “particulate” may also includean agglomeration comprising more than one individual particle,particulate, or the like. Additionally, a particle, particulate, or anydesired agglomeration thereof may be composed of more than one type ofmaterial.

The term “polymer” includes, but is not limited to, homopolymers,copolymers, for example, block, graft, random, and alternatingcopolymers, terpolymers, etc., and blends and modifications thereof.Furthermore, unless otherwise specifically limited, the term “polymer”shall include all possible configurational isomers of the material.These configurations include, but are not limited to isotactic,syndiotactic, and atactic symmetries.

The term “polyolefin” as used herein generally includes, but is notlimited to, materials such as polyethylene, polypropylene,polyisobutylene, polystyrene, ethylene vinyl acetate copolymer, and thelike, the homopolymers, copolymers, terpolymers, etc., thereof, andblends and modifications thereof. The term “polyolefin” shall includeall possible structures thereof, which include, but are not limited to,isotatic, synodiotactic, and random symmetries. Copolymers includeatactic and block copolymers.

The term “superabsorbent materials” refers to water-swellable,water-insoluble organic or inorganic materials including superabsorbentpolymers and superabsorbent polymer compositions capable, under the mostfavorable conditions, of absorbing at least about 10 times their weight,or at least about 15 times their weight, or at least about 25 timestheir weight in an aqueous solution containing 0.9 weight percent sodiumchloride.

The term “superabsorbent polymer composition” refers to a superabsorbentpolymer comprising a surface additive in accordance with the presentinvention.

The terms “superabsorbent polymer” and “superabsorbent polymerpreproduct” refer to a material that is produced by conducting all ofthe steps for making a superabsorbent polymer as described herein, up toand including drying the material, and coarse grinding in a crusher.

The term “superabsorbent polymer fines” refers to a fraction of fineparticles produced in the production process of superabsorbent polymers,having particles less than a certain size that may be about 300 microns,or about 200 microns, or about 150 microns.

The term “surface cross linking” means that the level of functionalcross links in the vicinity of the surface of the superabsorbent polymerparticle generally is higher than the level of functional cross links inthe interior of the superabsorbent polymer particle. As used herein,“surface” describes the outer-facing boundaries of the particle. Forporous superabsorbent polymer particles, exposed internal surface alsoare included in the definition of surface.

The term “thermoplastic” describes a material that softens when exposedto heat and which substantially returns to a non-softened condition whencooled to room temperature.

The term “% by weight” or “% wt” when used herein and referring tocomponents of the superabsorbent polymer composition, is to beinterpreted as based on the weight of the dry superabsorbent polymercomposition, unless otherwise specified herein.

These terms may be defined with additional language in the remainingportions of the specification.

DETAILED DESCRIPTION

An embodiment of the present invention comprises a process for theproduction of a superabsorbent polymer gel with recycled superabsorbentpolymer fines comprising the following steps: a) treating thesuperabsorbent polymer fines with a caustic solution containing fromabout 0.1 to about 12% caustic based on the weight of the superabsorbentpolymer fines; b) mixing the treated superabsorbent polymer finesobtained in step a) with a polymerization solution containing at leastone cross-linking-agent and a partially neutralized monomer in which thecontent of the superabsorbent polymer fines relative to the total amountof the monomer is from about 0.1 to about 30 wt %; and c) polymerizingthe mixture obtained in step b) to produce the superabsorbent polymergel.

In an embodiment of the present invention the superabsorbent polymerfines having an average particle size of less than about 300 μm, orabout 200 μm, or about 150 μm.

In addition, the process may further comprise the steps of separatingthe superabsorbent polymer fines from the superabsorbent polymercomposition particles, treating the superabsorbent polymer fines withcaustic such as sodium hydroxide, or sodium carbonate, or sodiumbicarbonate, and recycling the caustic treated superabsorbent polymerfines to the polymerizing step for forming said superabsorbent polymercomposition particles.

In another embodiment, the present invention is directed to a processfor the production of a superabsorbent polymer gel based on recyclingsuperabsorbent polymer fines comprising the following steps: a) treatingthe superabsorbent polymer fines with a caustic solution containing fromabout 0.1 to about 12% caustic based on the weight of the superabsorbentpolymer fines; b) mixing the treated superabsorbent polymer finesobtained in step a) with a polymerization solution containing at leastone cross-linking-agent and a monomer in which the content of thesuperabsorbent polymer fines relative to the total amount of the monomeris from about 0.1 to about 30 wt %; c) polymerizing the mixture obtainedin step b) to produce the polymer gel; and d) postneutralizing thepolymer gel to form a superabsorbent polymer gel.

In another embodiment, the present invention is directed to a processfor recycling superabsorbent polymer fines in the production ofsuperabsorbent polymer gel, compromising the steps of: a) treating thesuperabsorbent polymer fines with a caustic solution containing fromabout 0.1 to about 12% caustic based on the weight of the superabsorbentpolymer fines; b) mixing the treated superabsorbent polymer finesobtained in step a) with a polymerization solution containing at leastone cross-linking-agent and a partially neutralized monomer in which thecontent of the superabsorbent polymer fines relative to the total amountof the monomer is from about 0.1 to about 30 wt %; and c) polymerizingthe mixture obtained in step b) to produce a superabsorbent polymer gel.

In another embodiment, the present invention is directed to a processfor recycling for recycling superabsorbent polymer fines in theproduction of superabsorbent polymer gel, compromising the steps of: a)dissolving at least one acrylic acid monomer and/or its sodium salt anda cross-linking agent in an aqueous solution to form a monomer solution;b) polymerizing the mixture obtained in step a) to produce asuperabsorbent polymer gel. c) treating the superabsorbent polymer fineswith a caustic solution containing from about 0.1 to about 12% causticbased on the weight of the superabsorbent polymer fines; and d) mixingthe treated superabsorbent polymer fines obtained in step c) with thesuperabsorbent polymer gel obtained in step b) in which the content ofthe superabsorbent polymer fines relative to the total amount of thesuperabsorbent polymer gel is from about 0.1 to about 30 wt %.

A superabsorbent polymer as set forth in embodiments of the presentinvention is obtained by the initial polymerization of from about 55% toabout 99.9% by weight of the superabsorbent polymer of polymerizableunsaturated acid group containing monomer. A suitable monomer includesany of those containing carboxyl groups, such as acrylic acid,methacrylic acid, or 2-acrylamido-2-methylpropanesulfonic acid, ormixtures thereof. It is desirable for at least about 50% by weight, andmore desirable for at least about 75% by weight of the acid groups to becarboxyl groups.

The acid groups are neutralized to the extent of at least about 25mol %,that is, the acid groups are desirably present as sodium, potassium, orammonium salts. In some aspects, the degree of neutralization may be atleast about 50mol %. In some aspects, it is desirable to utilizepolymers obtained by polymerization of acrylic acid or methacrylic acid,the carboxyl groups of which are neutralized to the extent of from about50mol % to about 80mol %, in the presence of internal cross linkingagents.

In some aspects, the suitable monomer that can be copolymerized with theethylenically unsaturated monomer may include, but is not limited toacrylamide, methacrylamide, hydroxyethyl acrylate, dimethylaminoalkyl(meth)-acrylate, ethoxylated (meth)-acrylates,dimethylaminopropylacrylamide, or acrylamidopropyltrimethylammoniumchloride. Such monomer may be present in a range of from 0% to about 40%by weight of the copolymerized monomer.

The superabsorbent polymer of the invention also includes internal crosslinking agents. The internal cross linking agent has at least twoethylenically unsaturated double bonds, or one ethylenically unsaturateddouble bond and one functional group that is reactive toward acid groupsof the polymerizable unsaturated acid group containing monomer, orseveral functional groups that are reactive towards acid groups can beused as the internal cross linking component and is desirably presentduring the polymerization of the polymerizable unsaturated acid groupcontaining a monomer.

Examples of internal cross linking agents include, but are not limitedto, aliphatic unsaturated amides, such as methylenebisacryl- or-methacrylamide or ethylenebisacrylamide; aliphatic esters of polyols oralkoxylated polyols with ethylenically unsaturated acids, such asdi(meth)acrylates or tri(meth)acrylates of butanediol or ethyleneglycol, polyglycols or trimethylolpropane; di- and triacrylate esters oftrimethylolpropane which may be oxyalkylated, desirably ethoxylated,with about 1 to about 30 moles of alkylene oxide; acrylate andmethacrylate esters of glycerol and pentaerythritol and of glycerol andpentaerythritol oxyethylated with desirably about 1 to about 30mol ofethylene oxide; allyl compounds, such as allyl (meth)acrylate,alkoxylated allyl (meth)acrylate reacted with desirably about 1 to about30 mol of ethylene oxide, triallyl cyanurate, triallyl isocyanurate,maleic acid diallyl ester, poly-allyl esters, tetraallyloxyethane,triallylamine, tetraallylethylenediamine, diols, polyols, hydroxy allylor acrylate compounds and allyl esters of phosphoric acid or phosphorousacid; and monomers that are capable of cross linking, such as N-methylolcompounds of unsaturated amides, such as of methacrylamide oracrylamide, and the ethers derived therefrom. Ionic cross linkers suchas multivalent metal salts may also be employed. Mixtures of the crosslinking agents mentioned can also be employed. The content of theinternal cross linking agents is from about 0.001% to about 5% by weightsuch as from about 0.2% to about 3% by weight based on the total amountof the polymerizable unsaturated acid group containing monomer.

In some aspects, initiators can be used for initiation of thefree-radical polymerization. Suitable initiators include, but are notlimited to, azo or peroxo compounds, redox systems or UV initiators,sensitizers, and/or radiation.

After polymerization, the superabsorbent polymer is generally formedinto particles. The superabsorbent polymer particles may then be surfacecross linked after polymerization by the addition of a surface crosslinking agent and heat-treatment. In general, surface cross linking is aprocess that is believed to increase the cross link density of thepolymer matrix in the vicinity of the superabsorbent polymer particlesurface with respect to the cross linking density of the particleinterior.

In some particular aspects, desirable surface cross linking agentsinclude chemicals with one or more functional groups that are reactivetoward pendant groups of the polymer chains, typically the acid groups.The surface cross linking agent may be present in an amount of fromabout 0.001% to about 5% by weight of the dry superabsorbent polymercomposition, and such as from about 0.1% to about 3% by weight, and suchas from about 0.1% to about 1% by weight, based on the weight of the drysuperabsorbent polymer composition. Applicants have found that a heattreatment step after addition of the surface cross linking agent isdesirable.

In one particular aspect, the particulate superabsorbent polymer iscoated or surface-treated with an alkylene carbonate followed by heatingto affect surface cross linking, which can improve the surface crosslinking density and the gel strength characteristics of thesuperabsorbent polymer composition particle. More specifically, thesurface cross linking agent is coated onto the superabsorbent polymerparticulate by mixing the polymer particulate with an aqueous alcoholicsolution of the alkylene carbonate surface cross linking agent. Theamount of alcohol is determined by the solubility of the alkylenecarbonate and is kept as low as possible for various reasons. Suitablealcohols may include methanol, isopropanol, ethanol, butanol, or butylglycol, as well as mixtures of these alcohols. In some aspects, thesolvent desirably is water, which typically is used in an amount ofabout 0.3% by weight to about 5.0% by weight, based on the weight of thedry superabsorbent polymer composition. In other aspects, the alkylenecarbonate surface cross linking agent is dissolved in water without anyalcohol. In still other aspects, the alkylene carbonate surface crosslinking agent may be applied from a powder mixture, for example, with aninorganic carrier material, such as silicone dioxide (SiO₂), or in avapor state by sublimation of the alkylene carbonate.

To achieve the desired surface cross linking properties, the alkylenecarbonate is distributed evenly on the particulate superabsorbentpolymer. For this purpose, mixing is effected in suitable mixers knownin the art, such as fluidized bed mixers, paddle mixers, rotary drummixers, or twin-worm mixers. It is also possible to carry out thecoating of the particulate superabsorbent polymer during one of theprocess steps in the production of the particulate superabsorbentpolymer. In one particular aspect, a suitable process for this purposeis the inverse suspension polymerization process.

The heat treatment, that may follow the coating treatment, may becarried out as follows. In general, the heat treatment is at atemperature of from about 100° C. to about 300° C. Lower temperaturesare possible if highly reactive epoxide cross linking agents are used.However, if alkylene carbonates are used, then the thermal treatment issuitably at a temperature of from about 150° C. to about 250° C. In thisparticular aspect, the treatment temperature depends on the dwell timeand the kind of alkylene carbonate. For example, at a temperature ofabout 150° C., the thermal treatment is carried out for one hour orlonger. In contrast, at a temperature of about 250° C., a few minutes(e.g., from about 0.5 minutes to about 5 minutes) are sufficient toachieve the desired surface cross-linking properties. The thermaltreatment may be carried out in conventional dryers or ovens known inthe art.

In some aspects, the superabsorbent polymer composition of the presentinvention may include from 0% to about 5% by weight, or from about0.001% to about 5% by weight, or from about 0.01% to about 0.5% byweight of the dry superabsorbent polymer composition of a polymericcoating, such as a thermoplastic coating, or a cationic coating, or acombination of a thermoplastic coating and a cationic coating. In someparticular aspects, the polymeric coating desirably is a polymer thatmay be in a solid, emulsion, suspension, colloidal, or solubilizedstate, or combinations thereof. Polymeric coatings suitable for thisinvention may include, but are not limited to, a thermoplastic coatinghaving a thermoplastic melt temperature wherein the polymeric coating isapplied to the particle surface coincident with or followed by atemperature of the treated superabsorbent polymer particle at about thethermoplastic melt temperature.

Examples of thermoplastic polymers include, but are not limited to,polyolefin, polyethylene, polyester, polyamide, polyurethane, styrenepolybutadiene, linear low density polyethylene (LLDPE), ethylene acrylicacid copolymer (EAA), ethylene alkyl methacrylate copolymer (EMA),polypropylene (PP), maleated polypropylene, ethylene vinyl acetatecopolymer (EVA), polyester, polyamide, and blends of all families ofpolyolefins, such as blends of PP, EVA, EMA, EEA, EBA, HDPE, MDPE, LDPE,LLDPE, and/or VLDPE, may also be advantageously employed. The termpolyolefin as used herein is defined above. In particular aspects, theApplicants have found maleated polypropylene to be a desirablethermoplastic polymer for use in the present invention. A thermoplasticpolymer may be functionalized to have additional benefits such as watersolubility or dispersability.

Polymeric coatings of this invention may also include a cationicpolymer. A cationic polymer as used herein refers to a polymer ormixture of polymers comprising a functional group or groups having apotential of becoming positively charged ions upon ionization in anaqueous solution. Suitable functional groups for a cationic polymerinclude, but are not limited to, primary, secondary, or tertiary aminogroups, imino groups, imido groups, amido groups, and quaternaryammonium groups. Examples of synthetic cationic polymers include, butare not limited to, the salts or partial salts of poly(vinyl amines),poly(allylamines), poly(ethylene imine), poly(amino propanol vinylethers), poly(acrylamidopropyl trimethyl ammonium chloride),poly(diallyldimethyl ammonium chloride). Poly(vinyl amines) include, butare not limited to, LUPAMIN® 9095 available from BASF Corporation, MountOlive, N.J. Examples of natural-based cationic polymers include, but arenot limited to, partially deacetylated chitin, chitosan, and chitosansalts. Synthetic polypeptides such as polyasparagins, polylysines,polyglutamines, and polyarginines are also suitable cationic polymers.

The absorbent polymers according to the invention can comprise includefrom 0 to about 5 wt % of a multivalent metal salt, based on the weightof the mixture, on the surface of the polymer. The multivalent metalsalt is preferably water soluble. Examples of preferred metal cationsinclude the cations of Al, Fe, Zr, Mg and Zn. Preferably, the metalcation has a valence of at least +3, with Al being most preferred.Examples of preferred anions in the multivalent metal salt includehalides, chlorohydrates, sulfates, nitrates and acetates, withchlorides, sulfates, chlorohydrates and acetates being preferred,chlorohydrates and sulfates being more preferred and sulfates being themost preferred. Aluminum sulfate is the most preferred multivalent metalsalt and is readily commercially available. The preferred form ofaluminum sulfate is hydrated aluminum sulfate, preferably aluminumsulfate having from 12 to 14 waters of hydration. Mixtures ofmultivalent metal salts can be employed.

The polymer and multivalent metal salt suitably are mixed by dryblending, or preferably in solution, using means well known to thoseskilled in the art. Aqueous solutions are preferred. With dry blending,a binder may be employed in an amount which is sufficient to ensure thata substantially uniform mixture of the salt and the superabsorbentpolymer is maintained. The binder may be water or a nonvolatile organiccompound having a boiling point of at least 150° C. Examples of bindersinclude water, polyols such as propylene glycol, glycerin andpoly(ethylene glycol).

The superabsorbent polymer compositions according to the invention mayinclude from about 0.01% to about 2% by weight, or from about 0.01% toabout 1% by weight based on the dry superabsorbent polymer compositionof a water-insoluble inorganic metal compound. The water-insolubleinorganic metal compounds may include, but are not limited to, a cationselected from aluminum, titanium, calcium, or iron and an anion selectedfrom phosphate, borate, or sulfate. Examples of water-insolubleinorganic metal compounds include aluminum phosphate and an insolublemetal borate. The inorganic metal compound may have a mass medianparticle size of less than about 2 μm, and may have a mass medianparticle size of less than about 1 μm.

The inorganic metal compound can be applied in the dry physical form tothe surface of the superabsorbent polymer particles. For this, thesuperabsorbent polymer particles can be intimately mixed with the finelydivided inorganic metal compound. The finely divided inorganic metalcompound is usually added at about room temperature to thesuperabsorbent polymer particles and mixed in until a homogeneousmixture is present. For this purpose, mixing is effected in suitablemixers known in the art, such as fluidized bed mixers, paddle mixers,rotary drum mixers, or twin-worm mixers. The mixing of the SAP particleswith the finely divided water-insoluble inorganic metal compound maytake place before or after any surface cross linking, for example duringthe application of the surface cross linking agent.

Alternatively, a suspension of a finely divided water-insolubleinorganic metal compounds can be prepared and applied to a particulateSAP. The suspension is applied, for example, by spraying. Usefuldispersion media for preparing the suspension include water, organicsolvents such as alcohols, for example methanol, ethanol, isopropanol,ketones, for example acetone, methyl ethyl ketone, or mixtures of waterwith the aforementioned organic solvents. Other useful dispersion mediainclude dispersion aids, surfactants, protective colloidals, viscositymodifiers, and other auxiliaries to assist in the preparation of thesuspension. The suspension can be applied in conventional reactionmixers or mixing and drying systems as described above at a temperaturein the range from room temperature to less than the boiling point of thedispersion medium, preferably at about room temperature. It isappropriate to combine the application of the suspension with a surfacecross linking step by dispersing the finely divided water-insolublemetal salt in the solution of the surface cross linking agent.Alternatively, the suspension can also be applied before or after thesurface cross linking step. The application of the slurry may befollowed by a drying step.

In some aspects, the superabsorbent polymer compositions according tothe invention can include from 0% to about 5%, or from about 0.01% toabout 3%, by weight of the dry superabsorbent polymer composition ofsilica. Examples of silica include fumed silica, precipitated silica,silicon dioxide, silicic acid, and silicates. In some particularaspects, microscopic noncrystalline silicon dioxide is desirable.Products include SIPERNAT® 22S and AEROSIL® 200 available from EvonikCorporation, Parsippany, N.J. In some aspects, the particle diameter ofthe inorganic powder can be 1,000 μm or smaller, such as 100 μm orsmaller.

In some aspects, the superabsorbent polymer compositions may alsoinclude from 0% to about 30% by weight of the dry superabsorbent polymercomposition, such as from about 0.1% to about 5% by weight, ofwater-soluble polymers based by weight of the dry superabsorbent polymercomposition, of partly or completely hydrolyzed polyvinyl acetate,polyvinylpyrrolidone, starch or starch derivatives, polyglycols,polyethylene oxides, polypropylene oxides, or polyacrylic acids.

In some aspects, additional surface additives may optionally be employedwith the superabsorbent polymer particles, such as odor-bindingsubstances, such as cyclodextrins, zeolites, inorganic or organic salts,and similar materials; anti-caking additives, flow modification agents,surfactants, viscosity modifiers, and the like. In addition, surfaceadditives may be employed that perform several roles during surfacemodifications. For example, a single additive may be a surfactant,viscosity modifier, and may react to cross link polymer chains.

In some aspects, the superabsorbent polymer compositions of the presentinvention may be, after a heat treatment step, treated with water sothat the superabsorbent polymer composition has water content of up toabout 10% by weight of the superabsorbent polymer composition. Thiswater may be added with one or more of the surface additives from aboveadded to the superabsorbent polymer.

The superabsorbent polymer compositions according to the invention maybe prepared either continuously or discontinuously in a large-scaleindustrial manner, the after-cross linking according to the inventionbeing carried out accordingly. The partially neutralized monomer, suchas acrylic acid, is converted into a gel by free-radical polymerizationin aqueous solution in the presence of cross linking agents and anyfurther components, and the gel is comminuted, dried, ground, and sievedoff to the desired particle size. The superabsorbent polymer compositionparticles of the present invention generally include particle sizesranging from about 150 to about 850 microns. The present invention mayinclude at least about 40 wt % of the particles having a particle sizefrom about 300 μm to about 600 μm, or at least about 50 wt % of theparticles having a particle size from about 300 μm to about 600 μm, orat least about 60 wt % of the particles having a particle size fromabout 300 μm to about 600 μm as measured by screening through a U.S.standard 30 mesh screen and retained on a U.S. standard 50 mesh screen.In addition, the size distribution of the SAP particles of the presentinvention may include less than about 30% by weight of SAP particleshaving a size greater than about 600 microns, and less than about 30% byweight of SAP particles having a size of less than about 300 microns asmeasured using for example a RO-TAP® Mechanical Sieve Shaker Model Bavailable from W. S. Tyler, Inc., Mentor Ohio.

It is well known to those skilled in the art that particle sizedistribution of the SAP particles resembles a normal distribution or abell shaped curve. It is also known that for various reasons, the normaldistribution of the particle size distribution may be skewed in eitherdirection.

The SAP pre-product as used herein is produced by repeating all of thesteps for making the SAP particles, up to and including drying thematerial, and coarse grinding the superabsorbent polymer in a crusher,and removing superabsorbent polymer particles greater than about 850microns and smaller than about 150 microns. The particles smaller thanabout 300 μm, or about 200 μm, or about 150 μm are treated with acaustic solution and recycled in the polymerization process. The purposeof the caustic treatment is to partially hydrolyze the fines. Thetreated fines can be in slurry, paste, aggregate, or particulate forms.

In particular, treating the superabsorbent polymer fines with causticmay include a) treating the superabsorbent polymer fines with a causticsolution containing from about 0.1 to about 12 wt % caustic based on theweight of the fines aqueous solution. This can be done by mixing acaustic solution with superabsorbent polymer fines. For this purpose,mixing is effected in suitable mixers known in the art, such asfluidized bed mixers, paddle mixers, rotary drum mixers, or twin-wormmixers. The caustic solution is distributed evenly on the superabsorbentpolymer fines, for example, by spraying or dripping.

The treated superabsorbent polymer fines obtained in step a) is mixedwith a polymerization solution containing a cross-linking-agent and aneutralized monomer in which the content of the superabsorbent polymerfines relative to the total amount of monomers, amounts to 0.1 to 30 wt% and the mixture is polymerized to produce a superabsorbent polymergel. This process may further include the steps of comminuting theaqueous fluid absorbent polymer gel from said polymerizing step; dryingcommunicated polymer gel; separating the dried superabsorbent polymerparticle composition into a portion having a desired particle size fromabout 150 μm to about 850 μm. In addition, the steps may includeseparating the superabsorbent polymer fines having a particle size ofless than about 150 μm and recycling said superabsorbent polymer finesto the polymerizing step for forming said superabsorbent polymerparticle composition and treating the SAP fines with a caustic solution,and recycling the treated SAP fines in the monomer or gel.

In another embodiment of the present invention, the treatedsuperabsorbent polymer fines can be employed to increase the absorptionrate of superabsorbent polymer products when using a carbonate orbicarbonate containing solution to treat the fines, wherein the finesprovide a controllable delayed release of the carbonate or bicarbonateagent. It is well known in the art that carbonate or bicarbonatechemicals can act as blowing agents for superabsorbent polymers andcreate a microcellular expanded hydrogel, which gives fast absorptionrates. Treating the superabsorbent polymer fines with such blowingagents provides a controllable delayed release of a gas such as carbondioxide when dispersed in a monomer solution that is heated orpolymerized in accordance with the present invention. The controlledrelease of the blowing agent in the monomer solution allows control ofand improving the microcellular structure of the hydrogel.

The surface cross linked SAP product as used herein is produced byrepeating all of the steps for making the SAP particles, up to andincluding coating the material with a surface crosslinking agent andsurface additives, heating said coated polymer, and removingsuperabsorbent polymer particles greater than about 850 microns andsmaller than about 150 microns. The particles smaller than about 300 μm,or about 200 μm, or about 150 μm are treated with a caustic solution andrecycled in the polymerization process.

The superabsorbent polymer composition of the present invention exhibitscertain characteristics, or properties, as measured by Free Swell GelBed Permeability (GBP), Centrifuge Retention Capacity (CRC), absorbencyunder load at about 0.9 psi (AUL(0.9 psi)), and vortex time. The FreeSwell Gel Bed Permeability (GBP) Test is a measurement of thepermeability of a swollen bed of superabsorbent material in Darcy (e.g.,separate from the absorbent structure) under a confining pressure afterwhat is commonly referred to as “free swell” conditions. In thiscontext, the term “free swell” means that the superabsorbent material isallowed to swell without a swell restraining load upon absorbing testsolution as will be described. The Centrifuge Retention Capacity (CRC)Test measures the ability of the superabsorbent polymer composition toretain liquid therein after being saturated and subjected tocentrifugation under controlled conditions. The resultant retentioncapacity is stated as grams of liquid retained per gram weight of thesample (g/g).

The Absorbency Under Load (AUL) Test measures the ability of thesuperabsorbent polymer composition particles to absorb a 0.9 weightpercent solution of sodium chloride in distilled water at roomtemperature (test solution) while the material is under a load of 0.9psi. The vortex test measures the amount of time in seconds required for2 grams of a superabsorbent material to close a vortex created bystirring 50 milliliters of saline solution at 600 revolutions per minuteon a magnetic stir plate. The time it takes for the vortex to close isan indication of the free swell absorbing rate of the superabsorbentmaterial.

A superabsorbent polymer particulate composition made by a process ofpresent invention may have a centrifuge retention capacity of from about5 g/g to about 50 g/g, or from about 10 to about 45 g/g; and anabsorption under load at 0.9 psi of from about 10 g/g to about 26 g/g,or from about 13 to about 25 g/g, and a free swell gel bed permeabilityof from about 1 to about 70 Darcy.

The superabsorbent polymer compositions according to the presentinvention can be employed in many products including sanitary towels,diapers, or wound coverings, and they have the property that theyrapidly absorb large amounts of menstrual blood, urine, or other bodyfluids. Since the agents according to the invention retain the absorbedliquids even under pressure and are also capable of distributing furtherliquid within the construction in the swollen state, they are moredesirably employed in higher concentrations, with respect to thehydrophilic fiber material, such as fluff, when compared to conventionalcurrent superabsorbent compositions. They are also suitable for use as ahomogeneous superabsorber layer without fluff content within the diaperconstruction, as a result of which particularly thin articles arepossible. The polymers are furthermore suitable for use in hygienearticles (incontinence products) for adults.

The superabsorbent polymer compositions according to the invention mayalso be employed in absorbent articles that are suitable for furtheruses. In particular, the superabsorbent polymer compositions of thisinvention can be used in absorbent compositions for absorbents for wateror aqueous liquids, desirably in constructions for absorption of bodyfluids, in foamed and non-foamed sheet-like structures, in packagingmaterials, in constructions for plant growing, as soil improvementagents, or as active compound carriers. For this, they are processedinto a web by mixing with paper or fluff or synthetic fibers or bydistributing the superabsorbent polymer composition particles betweensubstrates of paper, fluff, or non-woven textiles, or by processing intocarrier materials. They are further suited for use in absorbentcompositions such as wound dressings, packaging, agriculturalabsorbents, food trays and pads, and the like.

The present invention may be better understood with reference to thefollowing examples.

Test Procedures

Centrifuge Retention Capacity Test

The Centrifuge Retention Capacity (CRC) Test measures the ability of thesuperabsorbent polymer to retain liquid therein after being saturatedand subjected to centrifugation under controlled conditions. Theresultant retention capacity is stated as grams of liquid retained pergram weight of the sample (g/g). The sample to be tested is preparedfrom particles that are pre-screened through a U.S. standard 30-meshscreen and retained on a U.S. standard 50-mesh screen. As a result, thesuperabsorbent polymer sample comprises particles sized in the range ofabout 300 to about 600 microns. The particles can be pre-screened byhand or automatically.

The retention capacity is measured by placing about 0.2 grams of thepre-screened superabsorbent polymer sample into a water-permeable bagthat will contain the sample while allowing a test solution (0.9 weightpercent sodium chloride in distilled water) to be freely absorbed by thesample. A heat-sealable tea bag material, such as that available fromDexter Corporation (having a place of business in Windsor Locks, Conn.,U.S.A.) as model designation 1234T heat sealable filter paper works wellfor most applications. The bag is formed by folding a 5-inch by 3-inchsample of the bag material in half and heat-sealing two of the openedges to form a 2.5-inch by 3-inch rectangular pouch. The heat seals areabout 0.25 inches inside the edge of the material. After the sample isplaced in the pouch, the remaining open edge of the pouch is alsoheat-sealed. Empty bags are also made to serve as controls. Threesamples are prepared for each superabsorbent polymer composition to betested.

The sealed bags are submerged in a pan containing the test solution atabout 23° C., making sure that the bags are held down until they arecompletely wetted. After wetting, the samples remain in the solution forabout 30 minutes, at which time they are removed from the solution andtemporarily laid on a non-absorbent flat surface.

The wet bags are then placed into the basket wherein the wet bags areseparated from each other and are placed at the outer circumferentialedge of the basket, wherein the basket is of a suitable centrifugecapable of subjecting the samples to a g-force of about 350. Onesuitable centrifuge is a CLAY ADAMS DYNAC II, model #0103, having awater collection basket, a digital rpm gauge, and a machined drainagebasket adapted to hold and drain the flat bag samples. Where multiplesamples are centrifuged, the samples are placed in opposing positionswithin the centrifuge to balance the basket when spinning. The bags(including the wet, empty bags) are centrifuged at about 1,600 rpm(e.g., to achieve a target g-force of about 290 g force with a variancefrom about 280 to about 300 g force), for 3 minutes. G force is definedas an unit of inertial force on a body that is subjected to rapidacceleration or gravity, equal to 32 ft/sec² at sea level. The bags areremoved and weighed, with the empty bags (controls) being weighed first,followed by the bags containing the superabsorbent polymer compositionsamples. The amount of solution retained by the superabsorbent polymersample, taking into account the solution retained by the bag itself, isthe centrifuge retention capacity (CRC) of the superabsorbent polymer,expressed as grams of fluid per gram of superabsorbent polymer. Moreparticularly, the retention capacity is determined by the followingequation:

$\mspace{11mu} \frac{\begin{matrix}{{{sample}\text{/}{bag}\mspace{14mu} {after}\mspace{14mu} {centrifuge}} - {{empty}\mspace{14mu} {bag}\mspace{14mu} {after}\mspace{14mu} {centrifuge}} -} \\{{dry}\mspace{14mu} {sample}\mspace{14mu} {weight}}\end{matrix}}{{dry}\mspace{14mu} {sample}\mspace{14mu} {weight}}\;$

The three samples are tested, and the results are averaged to determinethe Centrifuge Retention Capacity (CRC) of the superabsorbent polymercomposition.

Free-Swell Gel Bed Permeability Test (FSGBP)

As used herein, the Free-Swell Gel Bed Permeability Test, also referredto as the Gel Bed Permeability (GBP) Under 0 psi Swell Pressure Test,determines the permeability of a swollen bed of gel particles (e.g.,such as the surface treated absorbent material or the superabsorbentmaterial prior to being surface treated), under what is commonlyreferred to as “free swell” conditions. The term “free swell” means thatthe gel particles are allowed to swell without a restraining load uponabsorbing test solution as will be described. A suitable apparatus forconducting the Gel Bed Permeability Test is shown in FIGS. 1, 2 and 3and indicated generally as 500. The test apparatus assembly 528comprises a sample container, generally indicated at 530, and a plunger,generally indicated at 536. The plunger comprises a shaft 538 having acylinder hole bored down the longitudinal axis and a head 550 positionedat the bottom of the shaft. The shaft hole 562 has a diameter of about16 mm. The plunger head is attached to the shaft, such as by adhesion.Twelve holes 544 are bored into the radial axis of the shaft, threepositioned at every 90 degrees having diameters of about 6.4 mm. Theshaft 538 is machined from a LEXAN rod or equivalent material and has anouter diameter of about 2.2 cm and an inner diameter of about 16 mm.

The plunger head 550 has a concentric inner ring of seven holes 560 andan outer ring of 14 holes 554, all holes having a diameter of about 8.8millimeters as well as a hole of about 16 mm aligned with the shaft. Theplunger head 550 is machined from a LEXAN rod or equivalent material andhas a height of approximately 16 mm and a diameter sized such that itfits within the cylinder 534 with minimum wall clearance but stillslides freely. The total length of the plunger head 550 and shaft 538 isabout 8.25 cm, but can be machined at the top of the shaft to obtain thedesired mass of the plunger 536. The plunger 536 comprises a 100 meshstainless steel cloth screen 564 that is biaxially stretched to tautnessand attached to the lower end of the plunger 536. The screen is attachedto the plunger head 550 using an appropriate solvent that causes thescreen to be securely adhered to the plunger head 550. Care must betaken to avoid excess solvent migrating into the open portions of thescreen and reducing the open area for liquid flow. Acrylic solventWeld-on 4 from IPS Corporation (having a place of business in Gardena,Calif., USA) is a suitable solvent.

The sample container 530 comprises a cylinder 534 and a 400 meshstainless steel cloth screen 566 that is biaxially stretched to tautnessand attached to the lower end of the cylinder 534. The screen isattached to the cylinder using an appropriate solvent that causes thescreen to be securely adhered to the cylinder. Care must be taken toavoid excess solvent migrating into the open portions of the screen andreducing the open area for liquid flow. Acrylic solvent Weld-on 4 fromIPS Corporation (having a place of business in Gardena, Calif., USA) isa suitable solvent. A gel particle sample, indicated as 568 in FIG. 2,is supported on the screen 566 within the cylinder 534 during testing.

The cylinder 534 may be bored from a transparent LEXAN rod or equivalentmaterial, or it may be cut from a LEXAN tubing or equivalent material,and has an inner diameter of about 6 cm (e.g., a cross-sectional area ofabout 28.27 cm), a wall thickness of about 0.5 cm and a height ofapproximately 7.95 cm. A step is machined into the outer diameter of thecylinder 534 such that a region 534 a with an outer diameter of 66 mmexists for the bottom 31 mm of the cylinder 534. An o-ring 540 whichfits the diameter of region 534 a may be placed at the top of the step.

The annular weight 548 has a counter-bored hole about 2.2 cm in diameterand 1.3 cm deep so that it slips freely onto the shaft 538. The annularweight also has a thru-bore 548 a of about 16 mm. The annular weight 548can be made from stainless steel or from other suitable materialsresistant to corrosion in the presence of the test solution, which is0.9 weight percent sodium chloride solution in distilled water. Thecombined weight of the plunger 536 and annular weight 548 equalsapproximately 596 grams (g), which corresponds to a pressure applied tothe sample 568 of about 0.3 pounds per square inch (psi), or about 20.7dynes/cm² (2.07 kPa), over a sample area of about 28.27 cm.

When the test solution flows through the test apparatus during testingas described below, the sample container 530 generally rests on a weir600. The purpose of the weir is to divert liquid that overflows the topof the sample container 530 and diverts the overflow liquid to aseparate collection device 601. The weir can be positioned above a scale602 with a beaker 603 resting on it to collect saline solution passingthrough the swollen sample 568.

To conduct the Gel Bed Permeability Test under “free swell” conditions,the plunger 536, with the weight 548 seated thereon, is placed in anempty sample container 530 and the height from the top of the weight 548to the bottom of the sample container 530 is measured using a suitablegauge accurate to 0.01 mm. The force the thickness gauge applies duringmeasurement should be as low as possible, preferably less than about0.74 Newtons. It is important to measure the height of each empty samplecontainer 530, plunger 536, and weight 548 combination and to keep trackof which plunger 536 and weight 548 is used when using multiple testapparatus. The same plunger 536 and weight 548 should be used formeasurement when the sample 568 is later swollen following saturation.It is also desirable that the base that the sample cup 530 is resting onis level, and the top surface of the weight 548 is parallel to thebottom surface of the sample cup 530.

The sample to be tested is prepared from superabsorbent polymercomposition particles which are prescreened through a U.S. standard 30mesh screen and retained on a U.S. standard 50 mesh screen. As a result,the test sample comprises particles sized in the range of about 300 toabout 600 microns. The superabsorbent polymer particles can bepre-screened with, for example, a RO-TAP Mechanical Sieve Shaker Model Bavailable from W. S. Tyler, Inc., Mentor, Ohio. Sieving is conducted for10 minutes. Approximately 2.0 grams of the sample is placed in thesample container 530 and spread out evenly on the bottom of the samplecontainer. The container, with 2.0 grams of sample in it, without theplunger 536 and weight 548 therein, is then submerged in the 0.9% salinesolution for a time period of about 60 minutes to saturate the sampleand allow the sample to swell free of any restraining load. Duringsaturation, the sample cup 530 is set on a mesh located in the liquidreservoir so that the sample cup 530 is raised slightly above the bottomof the liquid reservoir. The mesh does not inhibit the flow of salinesolution into the sample cup 530. A suitable mesh can be obtained aspart number 7308 from Eagle Supply and Plastic, having a place ofbusiness in Appleton, Wis., U.S.A. Saline does not fully cover thesuperabsorbent polymer composition particles, as would be evidenced by aperfectly flat saline surface in the test cell. Also, saline depth isnot allowed to fall so low that the surface within the cell is definedsolely by swollen superabsorbent, rather than saline.

At the end of this period, the plunger 536 and weight 548 assembly areplaced on the saturated sample 568 in the sample container 530 and thenthe sample container 530, plunger 536, weight 548, and sample 568 areremoved from the solution. After removal and before being measured, thesample container 530, plunger 536, weight 548, and sample 568 are toremain at rest for about 30 seconds on a suitable flat, large gridnon-deformable plate of uniform thickness. The thickness of thesaturated sample 568 is determined by again measuring the height fromthe top of the weight 548 to the bottom of the sample container 530,using the same thickness gauge used previously provided that the zeropoint is unchanged from the initial height measurement. The samplecontainer 530, plunger 536, weight 548, and sample 568 may be placed ona flat, large grid non-deformable plate of uniform thickness that willprevent liquid in the sample container from being released onto a flatsurface due to surface tension. The plate has an overall dimension of7.6 cm by 7.6 cm, and each grid has a cell size dimension of 1.59 cmlong by 1.59 cm wide by 1.12 cm deep. A suitable flat, large gridnon-deformable plate material is a parabolic diffuser panel, cataloguenumber 1624K27, available from McMaster Carr Supply Company, having aplace of business in Chicago, Ill., U.S.A., which can then be cut to theproper dimensions. This flat, large mesh non-deformable plate must alsobe present when measuring the height of the initial empty assembly. Theheight measurement should be made as soon as practicable after thethickness gauge is engaged. The height measurement obtained frommeasuring the empty sample container 530, plunger 536, and weight 548 issubtracted from the height measurement obtained after saturating thesample 568. The resulting value is the thickness, or height “H” of theswollen sample.

The permeability measurement is initiated by delivering a flow of the0.9% saline solution into the sample container 530 with the saturatedsample 568, plunger 536, and weight 548 inside. The flow rate of testsolution into the container is adjusted to cause saline solution tooverflow the top of the cylinder 534 thereby resulting in a consistenthead pressure equal to the height of the sample container 530. The testsolution may be added by any suitable means that is sufficient to ensurea small, but consistent amount of overflow from the top of the cylinder,such as with a metering pump 604. The overflow liquid is diverted into aseparate collection device 601. The quantity of solution passing throughthe sample 568 versus time is measured gravimetrically using the scale602 and beaker 603. Data points from the scale 602 are collected everysecond for at least sixty seconds once the overflow has begun. Datacollection may be taken manually or with data collection software. Theflow rate, Q, through the swollen sample 568 is determined in units ofgrams/second (g/s) by a linear least-square fit of fluid passing throughthe sample 568 (in grams) versus time (in seconds).

Permeability in cm² is obtained by the following equation:K=[Q*H*μ]/[A*ρ*P], where K=Permeability (cm²), Q=flow rate (g/sec),H=height of swollen sample (cm), μ=liquid viscosity (poise)(approximately one centipoise for the test solution used with thisTest), A=cross-sectional area for liquid flow (28.27 cm² for the samplecontainer used with this Test), ρ=liquid density (g/cm³) (approximatelyone g/cm³, for the test solution used with this Test) and P=hydrostaticpressure (dynes/cm²) (normally approximately 7,797 dynes/cm²). Thehydrostatic pressure is calculated from P=ρ*g*h, where ρ=liquid density(g/cm³), g=gravitational acceleration, nominally 981 cm/sec², andh=fluid height, e.g., 7.95 cm for the Gel Bed Permeability Testdescribed herein.

A minimum of two samples is tested and the results are averaged todetermine the gel bed permeability of the sample.

Absorbency Under Load Test (AUL0.9 psi)

The Absorbency Under Load (AUL) Test measures the ability of thesuperabsorbent polymer composition particles to absorb a 0.9 weightpercent solution of sodium chloride in distilled water at roomtemperature (test solution) while the material is under a load of 0.9psi. The apparatus for testing AUL consists of:

-   -   An AUL assembly including a cylinder, a 4.4 g piston, and a        standard 317 gm weight. The components of this assembly are        described in additional detail below.    -   A flat-bottomed square plastic tray that is sufficiently broad        to allow the glass frits to lay on the bottom without contact        with the tray walls. A plastic tray that is 9″ by 9″(22.9        cm×22.9 cm), with a depth of 0.5 to 1″(1.3 cm to 2.5 cm) is        commonly used for this test method.    -   A 12.5 cm diameter sintered glass frit with a ‘C’ porosity        (25-50 microns). This frit is prepared in advance through        equilibration in saline (0.9% sodium chloride in distilled        water, by weight). In addition to being washed with at least two        portions of fresh saline, the frit must be immersed in saline        for at least 12 hours prior to AUL measurements.    -   Whatman Grade 1, 12.5 cm diameter filter paper circles.    -   A supply of saline (0.9% sodium chloride in distilled water, by        weight).

Referring to FIG. 4, the cylinder 412 of the AUL assembly 400 used tocontain the superabsorbent polymer composition particles 410 is madefrom one-inch (2.54 cm) inside diameter thermoplastic tubingmachined-out slightly to be sure of concentricity. After machining, a400 mesh stainless steel wire cloth 414 is attached to the bottom of thecylinder 412 by heating the steel wire cloth 414 in a flame until redhot, after which the cylinder 412 is held onto the steel wire clothuntil cooled. A soldering iron can be utilized to touch up the seal ifunsuccessful or if it breaks. Care must be taken to maintain a flatsmooth bottom and not distort the inside of the cylinder 412.

The 4.4 g piston (416) is made from one-inch diameter solid material(e.g., PLEXIGLAS®) and is machined to closely fit without binding in thecylinder 412.

A standard 317 gm weight 418 is used to provide a 62,053 dyne/cm² (about0.9 psi) restraining load. The weight is a cylindrical, 1 inch(2.5 cm)diameter, stainless steel weight that is machined to closely fit withoutbinding in the cylinder.

Unless specified otherwise, a sample 410 corresponding to a layer of atleast about 300 gsm. (0.16 g) of superabsorbent polymer compositionparticles is utilized for testing the AUL. The sample 410 is taken fromsuperabsorbent polymer composition particles that are pre-screenedthrough U.S. standard #30 mesh and retained on U.S. std. #50 mesh. Thesuperabsorbent polymer composition particles can be pre-screened with,for example, a RO-TAP® Mechanical Sieve Shaker Model B available from W.S. Tyler, Inc., Mentor, Ohio. Sieving is conducted for about 10 minutes.

The inside of the cylinder 412 is wiped with an antistatic cloth priorto placing the superabsorbent polymer composition particles 410 into thecylinder 412.

The desired amount of the sample of sieved superabsorbent polymercomposition particles 410 (about 0.16 g) is weighed out on a weigh paperand evenly distributed on the wire cloth 414 at the bottom of thecylinder 412. The weight of the superabsorbent polymer compositionparticles in the bottom of the cylinder is recorded as ‘SA,’ for use inthe AUL calculation described below. Care is taken to be sure nosuperabsorbent polymer particles cling to the wall of the cylinder.After carefully placing the 4.4 g piston 412 and 317 g weight 418 on thesuperabsorbent polymer composition particles 410 in the cylinder 412,the AUL assembly 400 including the cylinder, piston, weight, andsuperabsorbent polymer composition particles is weighed, and the weightis recorded as weight ‘A’.

A sintered glass frit 424 (described above) is placed in the plastictray 420, with saline 422 added to a level equal to that of the uppersurface of the glass frit 424. A single circle of filter paper 426 isplaced gently on the glass frit 424, and the AUL assembly 400 with thesuperabsorbent polymer composition particles 410 is then placed on topof the filter paper 426. The AUL assembly 400 is then allowed to remainon top of the filter paper 426 for a test period of one hour, withattention paid to keeping the saline level in the tray constant. At theend of the one hour test period, the AUL apparatus is then weighed, withthis value recorded as weight ‘B.’

The AUL(0.9 psi) is calculated as follows:

AUL(0.9 psi)=(B−A)/SA

wherein

A=Weight of AUL Unit with dry SAP

B=Weight of AUL Unit with SAP after 60 minutes absorption

SA=Actual SAP weight

A minimum of two tests is performed and the results are averaged todetermine the AUL value under 0.9 psi load. The samples are tested atabout 23° C. and about 50% relative humidity.

Vortex Time Test

The vortex test measures the amount of time in seconds required for 2grams of a superabsorbent material to close a vortex created by stirring50 milliliters of saline solution at 600 revolutions per minute on amagnetic stir plate. The time it takes for the vortex to close is anindication of the free swell absorbing rate of the superabsorbentmaterial.

Equipment and Materials

-   1. Schott Duran 100 ml Beaker and 50 ml graduated cylinder.-   2. Programmable magnetic stir plate, capable of providing 600    revolutions per minute (such as that commercially available from PMC    Industries, under the trade designation Dataplate® Model #721).-   3. Magnetic stir bar without rings, 7.9 millimeters.times.32    millimeters, Teflon® covered (such as that commercially available    from Baxter Diagnostics, under the trade designation S/PRIM. brand    single pack round stirring bars with removable pivot ring).-   4. Stopwatch-   5. Balance, accurate to ±0.01 g-   6. Saline solution, 0.87 w/w % Blood Bank Saline available from    Baxter Diagnostics (considered, for the purposes of this application    to be the equivalent of 0.9 wt. % saline-   7. Weighing paper-   8. Room with standard condition atmosphere: Temp =23° C.±1° C. and    Relative Humidity=50% ±2%.

Test Procedure

-   1. Measure 50 ml±0.01 ml of saline solution into the 100 ml beaker.-   2. Place the magnetic stir bar into the beaker.-   3. Program the magnetic stir plate to 600 revolutions per minute.-   4. Place the beaker on the center of the magnetic stir plate such    that the magnetic stir bar is activated. The bottom of the vortex    should be near the top of the stir bar.-   5. Weigh out 2 g ±0.01 g of the superabsorbent material to be tested    on weighing paper. NOTE: The superabsorbent material is tested as    received (i.e. as it would go into an absorbent composite such as    those described herein). No screening to a specific particle size is    done, though the particle size is known to have an effect on this    test.-   6. While the saline solution is being stirred, quickly pour the    superabsorbent material to be tested into the saline solution and    start the stopwatch. The superabsorbent material to be tested should    be added to the saline solution between the center of the vortex and    the side of the beaker.-   7. Stop the stopwatch when the surface of the saline solution    becomes flat and record the time.-   8. The time, recorded in seconds, is reported as the Vortex Time.

EXAMPLES

The following examples for the examples are provided to illustrate theinvention and do not limit the scope of the claims. Unless otherwisestated all parts, and percentages are by weight.

General Procedure for Preparing Superabsorbent Polymer Material andFines

It is generally understood that superabsorbent polymer fines may includeparticles having a particle size of about 150 μm or less, which may berecovering from the grinding process in making SAP particles. Thefollowing example provides information about making the SAP and fines.

Into a polyethylene vessel equipped with an agitator and cooling coilswas added, 2.0 kg of 50% NaOH to 3.32 kg of distilled water and cooledto 20° C. 0.8 kg of glacial acrylic acid was then added to the causticsolution and the solution again cooled to 20° C. 4.32 g of polyethyleneglycol monoallylether acrylate, 4.32 g of ethoxylated trimethylolpropane triacrylate SARTOMER® 454 product, and 1.6 kg of glacial acrylicacid were added to the first solution, followed by cooling to 4-6° C.Fines were added into the monomer solution with agitation. Nitrogen wasbubbled through the monomer solution for about 5 minutes. The monomersolution was then discharged into a rectangular tray. 80 g of 1% byweight of H₂O₂ aqueous solution, 120 g of 2 wt % aqueous sodiumpersulfate solution, and 72 g of 0.5 wt % aqueous sodium erythorbatesolution was added into the monomer solution to initiate polymerizationreaction. The agitator was stopped and the initiated monomer was allowedto polymerize for 20 minutes. The resulting hydrogel was chopped andextruded with a Hobart 4M6 commercial extruder, followed by drying in aProcter & Schwartz Model 062 forced air oven at 175° C. for 12 minuteswith up flow and 6 minutes with down flow air on a 20 in×40 inperforated metal tray to a final product moisture level of less than 5wt %. The dried material was coarse-ground in a Prodeva Model 315-Scrusher, milled in an MPI 666-F three-stage roller mill and sieved witha Minox MTS 600DS3V to remove particles greater than 850 μm and smallerthan 150 μm. The particles that are smaller than 150 microns are SAPfines.

The particles between 150 μm and 850 μm were coated with 1 wt % ofethylene carbonate, 3 wt % of water using a 25 wt % aqueous solution,and surface additives if applicable. The coated sample was then heatedin a convection oven at 185° C. for surface crosslinking. The surfacecrosslinked particulate material was then sieved with 20/100 mesh USstandard sieves to remove particles greater than 850 μm and smaller than150 μm. The particles that are smaller than 150 microns are surfacecrosslinked fines.

General Procedure for Treating Fines with Caustic Solutions

400 g of SAP fines were stirred in a Kitchen-Aid mixer. A Paascheairbrush sprayer was used to apply the caustic solutions, with the mixeron high speed while liquid was spraying. The treated fines were allowedto relax for at least 5 minutes prior to reworking into polymerizationbatches.

Examples 1, 2 and Comparative Example A

Surface crosslinked fines were treated with NaOH using a 50 wt % aqueoussolution. The treated fines were added into the monomer solution inwhich the content of the superabsorbent polymer fines relative to thetotal amount of the monomer solution is 1.9 wt % (5 wt % fines add-onbased on the dry weight of fines and the preproduct). In comparativeexample A, the untreated fines were added directly into the monomersolution. The results are summarized in Table 1 below. Compared with thepreproduct prepared with untreated fines, the products with treatedfines demonstrated higher CRC.

TABLE 1 NaOH add-on PSXM CRC Example Sample level (%) (g/g) Comparative233-21-2 0 38.6 Example A Example 1 233-8-4 6 41.8 Example 2 233-8-5 942.0 NaOH treatment level was based on the weight of NaOH solid andfines

Examples 3, 4 and Comparative Example B

The preproducts listed in Table 1 were coated with 1 wt % of ethylenecarbonate and 3 wt % of water, respectively. The coated sample was thenheated in a convection oven at 185° C. for surface crosslinking. Theresults are summarized in Table 2 below. Compared with the SXL productprepared with untreated fines, the products with treated finesdemonstrated higher 0.9 psi AUL.

TABLE 2 NaOH treatment SXL Time 0.9 psi Example level (%) (min) CRC(g/g) AUL (g/g) Comparative 0 30 33.3 17.9 Example B Example 3 6 40 34.621.1 Example 4 9 50 34 23.3 NaOH treatment level was based on the weightof NaOH solid and fines

Examples 5-8 and Comparative Examples C and D

The preproducts listed in Table 1 were coated with 0.5 wt % of Sipernat®22s, 1 wt % of ethylene carbonate, and 3 wt % of water, respectively.The coated sample was then heated in a convection oven at 185° C. forsurface crosslinking. The results are summarized in Table 3 below.Compared with the SXL products containing untreated fines, the productswith treated fines demonstrated higher 0.9 psi AUL and higher GBP.

TABLE 3 NaOH treatment SXM Time CRC 0.9 AUL GBP Example level (%) (min)(g/g) (g/g) (Darcy) Comparative 0 30 32.9 12.9 28.8 Example CComparative 0 40 31.9 14.1 38.4 Example D Example 5 6 40 32.8 15.3 47.7Example 6 6 50 31.8 16.1 59.4 Example 7 9 40 33.2 14.7 41.9 Example 8 950 32.8 16.4 48.2 NaOH treatment level was based on the weight of NaOHsolid and fines

Examples 9 and 10

Preproduct fines were treated with Na₂CO₃ using a 25 wt % aqueoussolution. The treated fines were added into the monomer solution inwhich the content of the superabsorbent polymer fines relative to thetotal amount of the monomer solution is 5.7 (15 wt % fines add-on basedon the dry weight of fines and preproduct). The results are summarizedin Table 4 below. The products prepared with Na₂CO₃ treated finesafforded fast absorption speed. Products prepared with untreated finesgenerally show the vortex time higher than 40 seconds.

TABLE 4 Na₂CO₃ treatment PSXM CRC Example level (%) (g/g) Vortex time(sec) Example 9 2.5 37.8 32 Example 10 5.0 34.2 22 Na₂CO₃ treatmentlevel was based on the weight of Na₂CO₃ solid and fines

Other than in the operating examples, or where otherwise indicated, allnumbers expressing quantities of ingredients, reaction conditions, andso forth used in the specification and claims are to be understood asbeing modified in all instances by the term “about.” Accordingly, unlessindicated to the contrary, the numerical parameters set forth in thefollowing specification and attached claims are approximations that mayvary depending upon the desired properties sought to be obtained by thepresent invention. At the very least, and not as an attempt to limit theapplication of the doctrine of equivalents to the scope of the claims,each numerical parameter should be construed in light of the number ofsignificant digits and ordinary rounding approaches.

Notwithstanding that the numerical ranges and parameters setting forththe broad scope of the invention are approximations, the numericalvalues set forth in the specific examples are reported as precisely aspossible. Any numerical value, however, inherently contain certainerrors necessarily resulting from the standard deviation found in theirrespective testing measurements.

1. A process for the production of a superabsorbent polymer gel withrecycled superabsorbent polymer fines comprising the following steps: a)treating the superabsorbent polymer fines with a caustic solutioncontaining from about 0.1 to about 12% caustic based on the weight ofthe superabsorbent polymer fines; b) mixing the treated superabsorbentpolymer fines obtained in step a) with a polymerization solutioncontaining at least one cross linking agent and a partially neutralizedmonomer in which the content of the superabsorbent polymer finesrelative to the total amount of the monomer is from about 0.1 to about30 wt %; and c) polymerizing the mixture obtained in step b) to producethe superabsorbent polymer gel.
 2. The process for the production ofsuperabsorbent polymer gel of claim 1 wherein the superabsorbent polymerfines having an average particle size of less than about 150 μm.
 3. Theprocess for the production of superabsorbent polymer gel of claim 2further comprising the steps to make a superabsorbent polymerparticulate wherein the steps comprise comminuting the aqueous fluidabsorbent polymer from said polymerizing step; drying said comminutedpolymer; separating said dried superabsorbent polymer particulate into aportion having a desired particle size from about 150 μm to about 850 μmas measured by screening through a U.S. standard 20 mesh screen andretained on a U.S. standard 100 mesh screen.
 4. The process for theproduction of superabsorbent polymer particulate of claim 3 furthercomprising the steps to make a superabsorbent polymer compositionwherein the steps comprise coating the superabsorbent polymer saidparticulate with a surface crosslinking agent and surface additives,heating said coated polymer, separating said dried superabsorbentpolymer particulate into a portion having a desired particle size fromabout 150 μm to about 850 μm as measured by screening through a U.S.standard 20 mesh screen and retained on a U.S. standard 100 mesh screen.5. The process for the production of superabsorbent polymer particulateof claim 3, further comprising the steps of separating thesuperabsorbent polymer fines having a particle size of less than about150 μm, treating the superabsorbent polymer fines with a causticsolution containing from about 0.1 to about 12% caustic based on theweight of the superabsorbent polymer fines, and recycling said treatedsuperabsorbent polymer fines to the polymerizing step for forming saidsuperabsorbent polymer gel.
 6. The process for the production ofsuperabsorbent polymer composition of claim 4 further comprising thesteps of separating the superabsorbent polymer fines having a particlesize of less than about 150 μm, treating the superabsorbent polymerfines with a caustic solution containing from about 0.1 to about 12%caustic based on the weight of the superabsorbent polymer fines, andrecycling said superabsorbent polymer fines to the polymerizing step forforming said superabsorbent polymer gel.
 7. The process for theproduction of superabsorbent polymer gel of claim 1 wherein the causticis sodium hydroxide.
 8. The process for the production of superabsorbentpolymer gel of claim 1 wherein the caustic is selected from sodiumcarbonate or sodium bicarbonate.
 9. The process for the production ofsuperabsorbent polymer particulate of claim 3 wherein the caustic isselected from sodium hydroxide, sodium carbonate or sodium bicarbonate.10. The process for the production of superabsorbent polymer particulateof claim 3 wherein said monomer is an ethylenically unsaturated monomersselected from amide, carboxylic acid or its esters, vinyl amines ortheir salts or mixtures thereof.
 11. The process for the production ofsuperabsorbent polymer gel of claim 1 wherein said polymer is a crosslinked polymer of polyacrylic acid, sodium polyacrylate or copolymersthereof.
 12. The process for the production of superabsorbent polymergel of claim 1 wherein said monomer solution includes an initiator. 13.A superabsorbent polymer particulate composition made by the process ofclaim 4 wherein at least about 40% by weight of the superabsorbentpolymer particulate has a particle size from about 300 μm to about 600μm as measured by screening through a U.S. standard 30 mesh screen andretained on a U.S. standard 50 mesh screen.
 14. The superabsorbentpolymer particulate composition of claim 13 having a centrifugeretention capacity of from about 10 g/g to about 45 g/g.
 15. Asuperabsorbent polymer particulate composition made by the process ofclaim 13 having an absorption under load at 0.9 psi of from about 13 g/gto about 26 g/g.
 16. A superabsorbent polymer particulate compositionmade by the process of claim 13 having a free swell gel bed permeabilityof from about 1 to about 70 Darcy.
 17. A superabsorbent polymerparticulate of claim 3 having a vortex time of about 40 seconds or less.18. An absorbent composition comprising the superabsorbent polymerparticle composition made by the process of claim
 4. 19. A sanitaryarticle comprising the superabsorbent polymer particle composition madeby the process of claim
 4. 20. A diaper comprising the superabsorbentpolymer particle composition made by the process of claim
 4. 21. Aprocess for the production of a superabsorbent polymer gel based onrecycling superabsorbent polymer fines comprising the following steps:a) treating the superabsorbent polymer fines with a caustic solutioncontaining from about 0.1 to about 12% caustic based on the weight ofthe superabsorbent polymer fines; b) mixing the treated superabsorbentpolymer fines obtained in step a) with a polymerization solutioncontaining at least one cross-linking-agent and a monomer in which thecontent of the superabsorbent polymer fines relative to the total amountof the monomer is from about 0.1 to about 30 wt %; c) polymerizing themixture obtained in step b) to produce the polymer gel; and d)postneutralizing the polymer gel to form a superabsorbent polymer gel.22. The process for the production of superabsorbent polymer gel ofclaim 21 wherein the superabsorbent polymer fines having an averageparticle size of less than about 150 μm.
 23. The process for theproduction of superabsorbent polymer gel of claim 22, further comprisingthe steps to make a superabsorbent polymer particulate wherein the stepscomprise comminuting the aqueous fluid absorbent polymer from saidpolymerizing step; drying said comminuted polymer; separating said driedsuperabsorbent polymer particulate into a portion having a desiredparticle size from about 150 ∞m to about 850 μm as measured by screeningthrough a U.S. standard 20 mesh screen and retained on a U.S. standard100 mesh screen.
 24. The process for the production of superabsorbentpolymer particulate of claim 23, further comprising the steps ofseparating the superabsorbent polymer fines having a particle size ofless than about 150 μm and recycling said superabsorbent polymer finesto the polymerizing step for forming said superabsorbent polymer gel.25. The process for the production of superabsorbent polymer particulateof claim 23 further comprising the steps to make a superabsorbentpolymer composition wherein the steps comprise coating thesuperabsorbent polymer said particulate with a surface crosslinkingagent and surface additives, heating said coated polymer, separatingsaid dried superabsorbent polymer particulate into a portion having adesired particle size from about 150 μm to about 850 μm as measured byscreening through a U.S. standard 20 mesh screen and retained on a U.S.standard 100 mesh screen.
 26. The process for the production ofsuperabsorbent polymer gel of claim 21 wherein the caustic is sodiumhydroxide.
 27. The process for the production of superabsorbent polymergel of claim 21 wherein the caustic is selected from sodium carbonate orsodium bicarbonate.
 28. The process for the production of superabsorbentpolymer gel of claim 25 wherein said polymer is a cross linked polymerof polyacrylic acid, sodium polyacrylate or copolymers thereof.
 29. Aprocess for recycling superabsorbent polymer fines in the production ofsuperabsorbent polymer gel, compromising the steps of: a) treating thesuperabsorbent polymer fines with a caustic solution containing fromabout 0.1 to about 12% caustic based on the weight of the superabsorbentpolymer fines; and b) mixing the treated superabsorbent polymer finesobtained in step a) with a polymerization solution containing at leastone cross-linking-agent and a partially neutralized monomer in which thecontent of the superabsorbent polymer fines relative to the total amountof the monomer is from about 0.1 to about 30 wt %; and c) polymerizingthe mixture obtained in step b) to produce a superabsorbent polymer gel.30. The process for recycling superabsorbent polymer fines in theproduction of superabsorbent polymer gel of claim 29 wherein thesuperabsorbent polymer fines having an average particle size of lessthan about 150 μm.
 31. The process for recycling superabsorbent polymerfines in the production of superabsorbent polymer gel of claim 30further comprising the steps to make a superabsorbent polymerparticulate wherein the steps comprise comminuting the aqueous fluidabsorbent polymer from said polymerizing step; drying said comminutedpolymer; separating said dried superabsorbent polymer particulate into aportion having a desired particle size from about 150 μm to about 850 μmas measured by screening through a U.S. standard 20 mesh screen andretained on a U.S. standard 100 mesh screen.
 32. The process forrecycling superabsorbent polymer fines in the production ofsuperabsorbent polymer gel of claim 31 further comprising the steps tomake a superabsorbent polymer composition wherein the steps comprisecoating the superabsorbent polymer particulate with a surfacecrosslinking agent and surface additives, heating said coated polymer,separating said dried superabsorbent polymer particulate into a portionhaving a desired particle size from about 150 μm to about 850 μm asmeasured by screening through a U.S. standard 20 mesh screen andretained on a U.S. standard 100 mesh screen.
 33. The process forrecycling superabsorbent polymer fines in the production ofsuperabsorbent polymer gel of claim 31, further comprising the steps ofseparating the superabsorbent polymer fines having a particle size ofless than about 150 μm and recycling said superabsorbent polymer finesto the polymerizing step for forming said superabsorbent polymer gel.34. The process for recycling superabsorbent polymer fines in theproduction of superabsorbent polymer gel of claim 32 further comprisingthe steps of separating the superabsorbent polymer fines having aparticle size of less than about 150 μm and recycling saidsuperabsorbent polymer fines to the polymerizing step for forming saidsuperabsorbent polymer gel.
 35. The process for recycling superabsorbentpolymer fines in the production of superabsorbent polymer gel of claim29 wherein the caustic is sodium hydroxide.
 36. The process forrecycling superabsorbent polymer fines in the production ofsuperabsorbent polymer gel of claim 29 wherein the caustic is selectedfrom sodium carbonate or sodium bicarbonate.
 37. The process forrecycling superabsorbent polymer fines in the production ofsuperabsorbent polymer gel of claim 29 wherein said monomer solutionincludes water-soluble ethylenically unsaturated monomer mixtures orsalts thereof.
 38. The process for recycling superabsorbent polymerfines in the production of superabsorbent polymer gel of claim 37wherein said ethylenically unsaturated monomer is an amide, carboxylicacid or its esters, vinyl amines or their salts or mixtures thereof. 39.The process for recycling superabsorbent polymer fines in the productionof superabsorbent polymer gel of claim 29 wherein said polymer is across linked polymer of polyacrylic acid, sodium polyacrylate orcopolymers thereof.
 40. The process for recycling superabsorbent polymerfines in the production of superabsorbent polymer gel of claim 29wherein said monomer solution includes an initiator.
 41. Asuperabsorbent polymer particulate composition made by the process ofclaim 32 wherein at least about 40% by weight of the superabsorbentpolymer particulate has a particle size from about 300 μm to about 600μm as measured by screening through a U.S. standard 30 mesh screen andretained on a U.S. standard 50 mesh screen.
 42. The superabsorbentpolymer particulate composition of claim 41 having a centrifugeretention capacity of from about 10 g/g to about 45 g/g.
 43. Asuperabsorbent polymer particulate composition made by the process ofclaim 41 having an absorption under load at 0.9 psi of from about 13 g/gto about 26 g/g.
 44. A superabsorbent polymer particulate compositionmade by the process of claim 41 having a free swell gel bed permeabilityof from about 1 to about 70 Darcy.
 45. A superabsorbent polymerparticulate of claim 32 having a vortex time of about 40 seconds orless.
 46. A process for recycling superabsorbent polymer fines in theproduction of superabsorbent polymer gel, compromising the steps of: a)dissolving at least one acrylic acid monomer and/or its sodium salt anda cross-linking agent in an aqueous solution to form a monomer solution;b) polymerizing the mixture obtained in step a) to produce asuperabsorbent polymer gel. c) treating the superabsorbent polymer fineswith a caustic solution containing from about 0.1 to about 12% causticbased on the weight of the superabsorbent polymer fines; and d) mixingthe treated superabsorbent polymer fines obtained in step c) with thesuperabsorbent polymer gel obtained in step b) in which the content ofthe superabsorbent polymer fines relative to the total amount of thesuperabsorbent polymer gel is from about 0.1 to about 30 wt %.
 47. Theprocess for recycling superabsorbent polymer fines in the production ofsuperabsorbent polymer gel of claim 46 wherein the superabsorbentpolymer fines having an average particle size of less than about 150 μm.48. The process for the production of superabsorbent polymer gel ofclaim 47 further comprising the steps to make a superabsorbent polymerparticulate wherein the steps comprise comminuting the aqueous fluidabsorbent polymer from said polymerizing and mixing step; drying saidcomminuted polymer; separating said dried superabsorbent polymerparticulate into a portion having a desired particle size from about 150μm to about 850 μm as measured by screening through a U.S. standard 20mesh screen and retained on a U.S. standard 100 mesh screen.
 49. Theprocess for the production of superabsorbent polymer particulate ofclaim 48 further comprising the steps to make a superabsorbent polymercomposition wherein the steps comprise coating the superabsorbentpolymer said particulate with a surface crosslinking agent and surfaceadditives, heating said coated polymer, separating said driedsuperabsorbent polymer particulate into a portion having a desiredparticle size from about 150 μm to about 850 μm as measured by screeningthrough a U.S. standard 20 mesh screen and retained on a U.S. standard100 mesh screen.
 50. The process for the production of superabsorbentpolymer particulate of claim 48, further comprising the steps ofseparating the superabsorbent polymer fines having a particle size ofless than about 150 μm, treating the superabsorbent polymer fines with acaustic solution containing from about 0.1 to about 12% caustic based onthe weight of the superabsorbent polymer fines, and recycling saidtreated superabsorbent polymer fines to the polymerizing step forforming said superabsorbent polymer gel.
 51. The process for theproduction of superabsorbent polymer composition of claim 49 furthercomprising the steps of separating the superabsorbent polymer fineshaving a particle size of less than about 150 μm, treating thesuperabsorbent polymer fines with a caustic solution containing fromabout 0.1 to about 12% caustic based on the weight of the superabsorbentpolymer fines, and recycling said superabsorbent polymer fines to thepolymerizing step for forming said superabsorbent polymer gel.
 52. Theprocess for the production of superabsorbent polymer gel of claim 46wherein the caustic is sodium hydroxide.
 53. The process for theproduction of superabsorbent polymer gel of claim 46 wherein the causticis selected from sodium carbonate or sodium bicarbonate.
 54. The processfor the production of superabsorbent polymer particulate of claim 48wherein the caustic is selected from sodium hydroxide, sodium carbonateor sodium bicarbonate.
 55. The process for the production ofsuperabsorbent polymer particulate of claim 48 wherein said monomer isan ethylenically unsaturated monomers selected from amide, carboxylicacid or its esters, vinyl amines or their salts or mixtures thereof. 56.The process for the production of superabsorbent polymer gel of claim 46wherein said polymer is a cross linked polymer of polyacrylic acid,sodium polyacrylate or copolymers thereof.
 57. The process for theproduction of superabsorbent polymer gel of claim 46 wherein saidmonomer solution includes an initiator.
 58. A superabsorbent polymerparticulate composition made by the process of claim 49 wherein at leastabout 40% by weight of the superabsorbent polymer particulate has aparticle size from about 300 μm to about 600 μm as measured by screeningthrough a U.S. standard 30 mesh screen and retained on a U.S. standard50 mesh screen.
 59. The superabsorbent polymer particulate compositionof claim 58 having a centrifuge retention capacity of from about 10 g/gto about 45 g/g.
 60. A superabsorbent polymer particulate compositionmade by the process of claim 58 having an absorption under load at 0.9psi of from about 13 g/g to about 26 g/g.
 61. A superabsorbent polymerparticulate composition made by the process of claim 58 having a freeswell gel bed permeability of from about 1 to about 70 Darcy.
 62. Asuperabsorbent polymer particulate of claim 48 having a vortex time ofabout 40 seconds or less.
 63. An absorbent composition comprising thesuperabsorbent polymer particle composition made by the process of claim49.
 64. A sanitary article comprising the superabsorbent polymerparticle composition made by the process of claim
 49. 65. A diapercomprising the superabsorbent polymer particle composition made by theprocess of claim 49.